A vapor-liquid-solid circulating fluidized bed, which is a new type of evap
oration boiling means for enhancing heat transfer and preventing fouling, i
s presented. Experiments were conducted in a 39 mm diameter 2.0 m high stai
nless steel column, in which the heat transfer coefficient was measured for
different superficial velocities, pressure of the heating stream, particle
concentration and kinds of particles. The experimental results show that t
he boiling heat transfer coefficient is enhanced and is about 1.5-2.0 times
that of vapor-liquid two-phase flow. The heat transfer coefficient increas
ed with increase in the pressure of the heating stream, but it exhibited a
local minimum value with increasing liquid velocity. (C) 2000 Elsevier Scie
nce S.A. All rights reserved.